Dual oxygen concentrator systems and methods

ABSTRACT

Described herein are various embodiments of an oxygen concentrator system that includes a home oxygen concentrator system couplable to a portable oxygen concentrator system.

PRIORITY CLAIM

This application claims priority to U.S. Provisional Application Ser. No. 61/713,254 entitled “Oxygen Concentrator Systems and Methods for Oral Delivery of Oxygen Enriched Air” filed Oct. 12, 2012, which is incorporated herein by reference in its entirety; and U.S. Provisional Application Ser. No. 61/804,368 entitled “Dual Oxygen Concentrator Systems and Methods for Oral Delivery of Oxygen Enriched Gas” filed Mar. 22, 2013, which is incorporated herein by reference in its entirety.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates generally to health equipment and, more specifically, to oxygen concentrators.

2. Description of the Related Art

There are many patients that require supplemental oxygen as part of Long Term Oxygen Therapy (LTOT). Currently, the vast majority of patients that are receiving LTOT are diagnosed under the general category of Chronic Obstructive Pulmonary Disease, COPD. This general diagnosis includes such common diseases as Chronic Asthma, Emphysema, Congestive Heart Failure and several other cardio-pulmonary conditions. Other people (e.g., obese individuals) may also require supplemental oxygen, for example, to maintain elevated activity levels.

Doctors may prescribe oxygen concentrators or portable tanks of medical oxygen for these patients. Usually a specific oxygen flow rate is prescribed (e.g., 1 liter per minute (LPM), 2 LPM, 3 LPM, etc.). Experts in this field have also recognized that exercise for these patients provide long term benefits that slow the progression of the disease, improve quality of life and extend patient longevity. Most stationary forms of exercise like tread mills and stationary bicycles, however, are too strenuous for these patients. As a result, the need for mobility has long been recognized. Until recently, this mobility has been facilitated by the use of small compressed oxygen tanks. The disadvantage of these tanks is that they have a finite amount of oxygen and they are heavy, weighing about 50 pounds, when mounted on a cart with dolly wheels.

Oxygen concentrators have been in use for about 50 years to supply patients suffering from respiratory insufficiency with supplemental oxygen. Traditional oxygen concentrators used to provide these flow rates have been bulky and heavy making ordinary ambulatory activities with them difficult and impractical. Recently, companies that manufacture large stationary home oxygen concentrators began developing portable oxygen concentrators, POCs. The advantage of POCs concentrators was that they can produce a theoretically endless supply of oxygen. In order to make these devices small for mobility, the various systems necessary for the production of oxygen enriched gas are condensed.

SUMMARY

Systems and methods of providing an oxygen enriched gas to a user of an oxygen concentrator are described herein.

In an embodiment, an oxygen concentrator system includes: a first oxygen concentrator and a second oxygen concentrator coupleable to the first oxygen concentrator. The first oxygen concentrator includes: at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a processor operable to execute program instructions. The second oxygen concentrator includes: at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; and a coupling system that couples the second oxygen concentrator apparatus to the first oxygen concentrator apparatus. In one embodiment, the first oxygen concentrator controller operates the first oxygen concentrator apparatus and, when the first oxygen concentrator is coupled to the second oxygen concentrator, the first oxygen concentrator controller controls operation of the second oxygen concentrator. The coupling system includes a support structure which has a size and shape complementary to the size and shape of the first oxygen concentrator.

The second oxygen concentrator system includes a power source cable that couples the second oxygen concentrator system to a power source during use. The coupling system includes a cord that electrically couples the second oxygen concentrator system to the first oxygen concentrator system. The first oxygen concentrator may include a rechargeable battery. The second oxygen concentrator may provide power to the battery of the first oxygen concentrator system such that the battery of the first oxygen concentrator is recharged when the first oxygen concentrator is coupled to the second oxygen concentrator.

In an embodiment, the second oxygen concentrator includes an oxygen enriched gas storage container, and one or more conduits that couple the oxygen enriched gas storage container to the first oxygen concentrator system such that oxygen enriched gas is provided to the first oxygen concentrator system from the oxygen enriched gas storage container. The conduits may couple the oxygen enriched gas storage container to an expansion chamber of the first oxygen concentrator system. Alternatively, the conduits may couple the outlet of one or more canisters of the second oxygen concentration system to an accumulator of the first oxygen concentrator system.

In one embodiment, the coupling system includes one or more conduits that couple the compressor of the first oxygen concentrator system to one or more of the canisters of the second oxygen concentrator system such that the compressor of the first oxygen concentrator system provides compressed air to one or more of the conduits of the second oxygen concentrator system when the first oxygen concentrator system is coupled to the second oxygen concentrator system. In an embodiment, the conduits couple the outlet of one or more canisters of the second oxygen concentration system to the first oxygen concentrator system such that oxygen enriched gas is provided to the first oxygen concentrator system from the second oxygen concentrator system. In an embodiment, the conduits couple the outlet of one or more canisters of the second oxygen concentration system to an outlet conduit of the first oxygen concentration system that provides oxygen to a user of the first oxygen concentrator system

In one embodiment, a separate controller is coupleable to the second oxygen concentrator system via the coupling system, wherein the separate controller operates the second oxygen concentrator system. The second oxygen concentrator may include a compression system. The first oxygen concentrator controller, or the separate controller may operate the second oxygen concentrator compression system.

In an embodiment, a method of providing oxygen enriched gas to a user of an oxygen concentrator includes coupling a first oxygen concentrator apparatus to a second oxygen concentrator apparatus and using the first oxygen concentrator system to operate the second oxygen concentrator to provide oxygen enriched gas to the user from the second oxygen concentrator. The first oxygen concentrator apparatus includes: at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a controller capable of sending control signals to operate components of the first and second oxygen concentrator systems. The second oxygen concentrator system includes at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; and a coupling system that couples the second oxygen concentrator apparatus to the first oxygen concentrator apparatus. In an embodiment, the first and second oxygen concentrators are controlled using a controller of the first oxygen concentrator. The first and second oxygen concentrators may be controlled by transmitting a signal from a wireless controller of the first oxygen concentrator to the second oxygen concentrator.

The method also includes regenerating gas separation adsorbent in the first oxygen concentrator system while providing oxygen enriched gas to the user from the second oxygen concentrator.

In an embodiment, a method of providing oxygen enriched gas to a user of an oxygen concentrator, includes coupling a first oxygen concentrator apparatus to a second oxygen concentrator apparatus. The first oxygen concentrator apparatus includes: at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a first apparatus controller that controls operation of the first oxygen concentrator apparatus using operating parameters stored in the first apparatus controller. The second oxygen concentrator apparatus includes: at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a second apparatus controller that controls operation of the second oxygen concentrator apparatus using operating parameters stored in the second apparatus controller. The first apparatus controller is coupled to the second apparatus controller when the first oxygen concentrator apparatus is coupled to the second oxygen concentration apparatus. The method includes altering the operating parameters of the second apparatus controller based on the operating parameters of the first apparatus controller when the first oxygen concentrator system is coupled to the second oxygen concentrator system. The operating parameters of the second apparatus controller are altered by the first apparatus controller.

In an embodiment an oxygen concentrator system, includes: a first oxygen concentrator apparatus and a second oxygen concentrator apparatus. The first oxygen concentrator apparatus includes: at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a first apparatus controller that controls the operation of the first oxygen concentrator apparatus. The second oxygen concentrator apparatus includes: at least two canisters; gas separation adsorbent disposed in at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; a second apparatus controller that controls the operation of the second oxygen concentrator apparatus using operating parameters stored in the second apparatus controller; and a coupling system that couples the first apparatus controller to the second apparatus controller. The first apparatus controller alters the operating parameters of the second apparatus controller when coupled to the second apparatus controller.

BRIEF DESCRIPTION OF THE DRAWINGS

Advantages of the present invention will become apparent to those skilled in the art with the benefit of the following detailed description of embodiments and upon reference to the accompanying drawings in which:

FIG. 1 depicts a projection view of an embodiment of a hybrid oxygen concentrator system.

FIG. 2 depicts a schematic diagram of a portable oxygen concentrator coupled to a home oxygen concentrator of a hybrid oxygen concentrator system, shown in FIG. 1.

FIG. 3 depicts a schematic diagram of an embodiment of the outlet components of an oxygen concentrator.

FIG. 4 depicts a schematic diagram of an embodiment of an outlet conduit for an oxygen concentrator;

FIG. 5 depicts a perspective view of an embodiment of a dissembled canister system;

FIG. 6 depicts an end view of an embodiment of an end of a canister system.

FIG. 7 depicts the assembled end of an embodiment of the canister system end depicted in FIG. 6.

FIG. 8 depicts an end view of an embodiment of an opposing end of the canister system depicted in FIG. 5.

FIG. 9 depicts an end view of an embodiment of the assembled opposing end of the canister system end depicted in FIG. 8.

FIG. 10 depicts various profiles of embodiments for providing oxygen enriched gas from an oxygen concentrator.

FIG. 11 depicts a schematic diagram of a portable oxygen concentrator to a home oxygen concentrator that does not have a compressor system.

FIG. 12 depicts a perspective view of a home concentrator system having a removable control panel.

While the invention is susceptible to various modifications and alternative forms, specific embodiments thereof are shown by way of example in the drawings and will herein be described in detail. It should be understood, however, that the drawings and detailed description thereto are not intended to limit the invention to the particular form disclosed, but on the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the present invention as defined by the appended claims.

DETAILED DESCRIPTION

It is to be understood the present invention is not limited to particular devices or methods, which may, of course, vary. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting. Headings are for organizational purposes only and are not meant to be used to limit or interpret the description or claims. As used in this specification and the appended claims, the singular forms “a”, “an”, and “the” include singular and plural referents unless the content clearly dictates otherwise. Furthermore, the word “may” is used throughout this application in a permissive sense (i.e., having the potential to, being able to), not in a mandatory sense (i.e., must). The term “include,” and derivations thereof, mean “including, but not limited to.”

The term “coupled” as used herein means either a direct connection or an indirect connection (e.g., one or more intervening connections) between one or more objects or components. The phrase “connected” means a direct connection between objects or components such that the objects or components are connected directly to each other. As used herein the phrase “obtaining” a device means that the device is either purchased or constructed.

Oxygen concentrators take advantage of pressure swing adsorption (PSA). Pressure swing adsorption involves using a compressor to increase gas pressure inside a canister that contains particles of a gas separation adsorbent. As the pressure increases, certain molecules in the gas may become adsorbed onto the gas separation adsorbent. Removal of a portion of the gas in the canister under the pressurized conditions allows separation of the non-adsorbed molecules from the adsorbed molecules. The gas separation adsorbent may be regenerated by reducing the pressure, which reverses the adsorption of molecules from the adsorbent. Further details regarding oxygen concentrators may be found, for example, in U.S. Published Patent Application No. 2009-0065007, published Mar. 12, 2009, and entitled “Oxygen Concentrator Apparatus and Method”, which is incorporated herein by reference.

Ambient air usually includes approximately 78% nitrogen and 21% oxygen with the balance comprised of argon, carbon dioxide, water vapor and other trace elements. If a gas mixture such as air, for example, is passed under pressure through a vessel containing a gas separation adsorbent bed that attracts nitrogen more strongly than it does oxygen, part or all of the nitrogen will stay in the bed, and the gas coming out of the vessel will be enriched in oxygen. When the bed reaches the end of its capacity to adsorb nitrogen, it can be regenerated by reducing the pressure, thereby releasing the adsorbed nitrogen. It is then ready for another cycle of producing oxygen enriched air. By alternating canisters in a two-canister system, one canister can be collecting oxygen while the other canister is being purged (resulting in a continuous separation of the oxygen from the nitrogen). In this manner, oxygen can be accumulated out of the air for a variety of uses include providing supplemental oxygen to patients.

Users of oxygen concentrators may have a home oxygen concentrator and a portable oxygen concentrator. While portable oxygen concentrators provide many conveniences for a user, the battery life is limited. Thus, most users have a stationary oxygen concentrator for use at night or at home. The portable oxygen concentrator may be recharged while a user is using a stationary oxygen concentrator. A stationary oxygen concentrator may have an electrical power source and/or more or larger canisters of gas separation adsorbent that allows the unit to be used for longer periods of time. Many stationary units are large, heavy, and expensive. Thus, it is desirable to have an oxygen concentrator system that is suitable as a stationary and portable unit.

A hybrid portable oxygen concentrator system is described herein. FIG. 1 depicts a see-through projection view of a hybrid oxygen concentrator system 700. Hybrid oxygen concentrator system 700 may include portable oxygen concentrator 100, home oxygen concentrator 720, and coupler 750. Coupler 750 (dock) may be any type of coupler that allows portable oxygen concentrator 100 and home oxygen concentrator 720 to share electrical power and/or electrical signals.

FIG. 2 depicts a schematic diagram of a portable oxygen concentrator 100 coupled to a home oxygen concentrator 720. Portable oxygen concentrator 100 includes: at least two canisters 302/304; a gas separation adsorbent disposed in the at least two canisters (not depicted); a compression system 200 and a controller (processor) 400. Home oxygen concentrator system includes: at least two canisters 730; a gas separation adsorbent disposed in the at least two canisters (not depicted); a coupler 750 that couples the portable oxygen concentrator to the home oxygen concentrator, and a compression system 780.

Coupler 750, in one embodiment, may include a support structure 752 which has a size and shape complementary to the shape of the portable oxygen concentrator system 100. In an embodiment, portable oxygen concentrator system 100 may be at least partially disposed within support structure 752. Support member 752 may be pivotable between an open position and a closed position. In the open position (as depicted in FIG. 15), the portable oxygen concentrator system may be placed in support member 752. After portable oxygen concentrator 100 is placed in support member 752, support member 752 may be moved into a closed position, which retains the portable oxygen concentrator system within home oxygen concentrator system 720.

Home oxygen concentrator 720 may be made of molded plastic or other suitable light weight material. In some embodiments, home oxygen concentrator 720 includes wheels 740 (which may be retractable) that allow the home oxygen concentrator to be moved. Supports 745 may be used to inhibit unintentional movement of the home oxygen concentrator. Thus, in one embodiment, home oxygen concentrator 720 may only be moved if the home oxygen concentrator is tilted, such that supports 745 are no longer in contact with the ground.

One advantage of the above described hybrid oxygen concentrator system 700 is that, when a user is at home, the home oxygen concentrator may be used to provide oxygen to the user. This reduces the amount of time the portable oxygen concentrator is used, prolonging the life of the portable oxygen concentrator. For example, by using the home oxygen concentrator to supply oxygen enriched gas to the user, the life of the canisters and batteries of the portable oxygen concentrator is prolonged, since these components are not used when at home. One problem of using prior art home oxygen concentrators is that such systems generally have controllers that are required to be independently programmed. A user having both a home oxygen concentrator and a portable oxygen concentrator, will typically need to program each device separately. Each of the devices must be programmed independently, when the prescription information for the user changes. This can lead to problems in which a home oxygen concentrator provides oxygen according to different parameters than the portable oxygen concentrator, leading to medical problems.

In one embodiment, portable oxygen concentrator 100 includes a controller than controls the operation of the portable oxygen concentrator. When the portable oxygen concentrator 100 is coupled to the home oxygen concentrator 720, the portable oxygen concentrator controller controls the operation of the home oxygen concentrator (e.g., the compression system, valves and oxygen delivery). This allows a user to only need to program one controller (in this example, the portable oxygen concentrator controller). Since portable oxygen concentrator 100 is always with the user, it will always have the most updated prescription and oxygen delivery information, customized for the user. In this embodiment, home oxygen concentrator 720 does not need a controller, or at most, a minimal controller that can receive and process control signals from the portable oxygen concentrator controller. The use of a shared controller helps to minimize the costs of the home oxygen concentrator, by eliminating the need for a costly controller to be installed on the home oxygen concentrator system.

Home oxygen concentrator 720 includes a power supply 726. Power supply 726 includes a power source cable (not shown) which couples the power supply to a power source. For example, home oxygen concentrator may include a power source cable that plugs into a wall socket. When portable oxygen concentrator 100 is coupled to stationary oxygen concentrator, one or more batteries of portable oxygen concentrator may be recharged. A cable 722 may couple portable oxygen concentrator 100 to home oxygen concentrator. Cable 722 may transmit power from power supply 726 to one or more batteries of portable oxygen concentrator 100. The power supplied to the batteries may be used to recharge one or more of the batteries when the portable oxygen concentrator is coupled to the home concentrator system.

In one embodiment, home oxygen concentrator 720 does not include a compressor or a controller. In such an embodiment, home oxygen concentrator 720 includes at least two canisters and a gas separation adsorbent disposed in the at least two canisters. Home oxygen concentrator 720 also includes one or more conduits that couple the canisters to portable oxygen concentrator 100, when the portable oxygen concentrator is coupled to the home oxygen concentrator. When coupled to the home oxygen concentrator, the portable oxygen concentrator acts as the controller and the compressor for the system. When a user requires oxygen enriched gas from the docked system, the user operates the portable oxygen concentrator to signal that the user is need of oxygen enriched gas (e.g., by turning the portable oxygen concentrator on). In response to the user's request for oxygen enriched gas, the portable oxygen concentrator turns on the portable oxygen concentrator compressors and provides compressed air to the canisters of the home oxygen concentrator.

After compressed air is converted into oxygen enriched air the oxygen enriched air is transferred to the portable oxygen concentrator. The oxygen enriched air is then provided to the user via the portable oxygen concentrator. In some embodiments, the oxygen enriched air produced in the home oxygen concentrator is provided to an accumulator of the portable oxygen concentrator, where the oxygen is stored until needed by the user. Alternatively, home oxygen concentrator 720 may include an accumulator 735 which stores the oxygen produced in the canisters of the home oxygen concentrator. Portable oxygen concentrator controller may control one or more valves (either disposed in the portable oxygen concentrator or disposed in the home oxygen concentrator) to cycle the gases through the canisters in a manner the same as, or similar to, the cycle used in the portable oxygen concentrator.

FIG. 2 illustrates a schematic diagram of a portable oxygen concentrator 100 coupled to a home oxygen concentrator 720, according to an embodiment. Oxygen concentrators 100 and 720 may concentrate oxygen out of an air stream to provide oxygen enriched gas to a user. As used herein, “oxygen enriched gas” is composed of at least about 50% oxygen, at least about 60% oxygen, at least about 70% oxygen, at least about 80% oxygen, at least about 90% oxygen, at least about 95% oxygen, at least about 98% oxygen, or at least about 99% oxygen.

Oxygen concentrator 100 may be a portable oxygen concentrator. For example, oxygen concentrator 100 may have a weight and size that allows the oxygen concentrator to be carried by hand and/or in a carrying case. In one embodiment, oxygen concentrator 100 has a weight of less than about 20 lbs., less than about 15 lbs., less than about 10 lbs., or less than about 5 lbs. In an embodiment, oxygen concentrator 100 has a volume of less than about 1000 cubic inches, less than about 750 cubic inches; less than about 500 cubic inches, less than about 250 cubic inches, or less than about 200 cubic inches.

Oxygen may be collected from ambient air by pressurizing ambient air in canisters 302 and 304, which include a gas separation adsorbent. Gas separation adsorbents useful in an oxygen concentrator are capable of separating at least nitrogen from an air stream to produce oxygen enriched gas. Examples of gas separation adsorbents include molecular sieves that are capable of separation of nitrogen from an air stream. Examples of adsorbents that may be used in an oxygen concentrator include, but are not limited to, zeolites (natural) or synthetic crystalline aluminosilicates that separate nitrogen from oxygen in an air stream under elevated pressure. Examples of synthetic crystalline aluminosilicates that may be used include, but are not limited to: OXYSIV adsorbents available from UOP LLC, Des Plaines, Iowa; SYLOBEAD adsorbents available from W. R. Grace & Co, Columbia, Md.; SILIPORITE adsorbents available from CECA S.A. of Paris, France; ZEOCHEM adsorbents available from Zeochem AG, Uetikon, Switzerland; and AgLiLSX adsorbent available from Air Products and Chemicals, Inc., Allentown, Pa.

As shown in FIG. 2, air may enter the portable oxygen concentrator through air inlet 106. Air may be drawn into air inlet 106 by compression system 200. Compression system 200 may draw in air from the surroundings of the portable oxygen concentrator and compress the air, forcing the compressed air into one or both canisters 302 and 304. In an embodiment, an inlet muffler 108 may be coupled to air inlet 106 to reduce sound produced by air being pulled into the oxygen generator by compression system 200. In an embodiment, inlet muffler 108 may be a moisture and sound absorbing muffler. For example, a water absorbent material (such as a polymer water absorbent material or a zeolite material) may be used to both absorb water from the incoming air and to reduce the sound of the air passing into the air inlet 106.

Compression system 200 may include one or more compressors capable of compressing air. In some embodiments, compression system may include one, two, three, four, or more compressors. Pressurized air, produced by compression system 200, may be forced into one or both of the canisters 302 and 304. In some embodiments, the ambient air may be pressurized in the canisters to a pressure approximately in a range of 13-20 pounds per square inch (psi). Other pressures may also be used, depending on the type of gas separation adsorbent disposed in the canisters.

In some embodiments, the compression system may include a motor coupled to a pressurizing device (e.g. piston pump or a diaphragm pump). The pressuring device may be a piston pump that has multiple pistons. During operation, the pistons may be selectively turned on or off. In some embodiments, the motor may be coupled to multiple pumps. Each pump may be selectively turned on or off. For example, controller 400 may determine which pumps or pistons should be operated based on predetermined operating conditions.

Coupled to each canister 302/304 are inlet valves 122/124 and outlet valves 132/134. As shown in FIG. 2, inlet valve 122 is coupled to canister 302 and inlet valve 124 is coupled to canister 304. Outlet valve 132 is coupled to canister 302 and outlet valve 134 is coupled to canister 304. Inlet valves 122/124 are used to control the passage of air from compression system 200 to the respective canisters. Outlet valves 132/134 are used to release gas from the respective canisters during a venting process. In some embodiments, inlet valves 122/124 and outlet valves 132/134 may be silicon plunger solenoid valves. Other types of valves, however, may be used. Plunger valves offer advantages over other kinds of valves by being quiet and having low slippage.

In some embodiments, a two-step valve actuation voltage may be used to control inlet valves 122/124 and outlet valves 132/134. For example, a high voltage (e.g., 24 V) may be applied to an inlet valve to open the inlet valve. The voltage may then be reduced (e.g., to 7 V) to keep the inlet valve open. Using less voltage to keep a valve open may use less power (Power=Voltage*Current). This reduction in voltage minimizes heat buildup and power consumption to extend run time from the battery. When the power is cut off to the valve, it closes by spring action. In some embodiments, the voltage may be applied as a function of time that is not necessarily a stepped response (e.g., a curved downward voltage between an initial 24 V and a final 7 V).

In some embodiments, air may be pulled into the oxygen concentrator through compressors 305, 310. In some embodiments, air may flow from compressors 305, 310 to canisters 302, 304. In some embodiments, one of valves 122 or 124 may be closed (e.g., as signaled by controller 400) resulting in the combined output of both compressors 305, 310 lowing through the other respective valve 122 or 124 into a respective canister 302, 304. For example, if valve 124 is closed, the air from both compressors 305, 310 may flow through valve 122. If valve 122 is closed, the air from both compressors 305, 310 may flow through valve 124. In some embodiments, valve 122 and valve 124 may alternate to alternately direct the air from the compressors 305, 310 into respective canisters 302 or 304.

In an embodiment, pressurized air is sent into one of canisters 302 or 304 while the other canister is being vented. For example, during use, inlet valve 122 is opened while inlet valve 124 is closed. Pressurized air from compression system 200 is forced into canister 302, while being inhibited from entering canister 304 by inlet valve 124. In an embodiment, a controller 400 is electrically coupled to valves 122, 124, 132, and 134. Controller 400 includes one or more processors 410 operable to execute program instructions stored in memory 420. The program instructions are operable to perform various predefined methods that are used to operate the oxygen concentrator. Controller 400 may include program instructions for operating inlet valves 122 and 124 out of phase with each other, i.e., when one of inlet valves 122 or 124 is opened, the other valve is closed. During pressurization of canister 302, outlet valve 132 is closed and outlet valve 134 is opened. Similar to the inlet valves, outlet valves 132 and 134 are operated out of phase with each other. In some embodiments, the voltages and the duration of the voltages used to open the input and output valves may be controlled by controller 400.

Check valves 142 and 144 are coupled to canisters 302 and 304, respectively. Check valves 142 and 144 are one way valves that are passively operated by the pressure differentials that occur as the canisters are pressurized and vented. Check valves 142 and 144 are coupled to canisters to allow oxygen produced during pressurization of the canister to flow out of the canister, and to inhibit back flow of oxygen or any other gases into the canister. In this manner, check valves 142 and 144 act as one way valves allowing oxygen enriched gas to exit the respective canister during pressurization.

The term “check valve”, as used herein, refers to a valve that allows flow of a fluid (gas or liquid) in one direction and inhibits back flow of the fluid. Examples of check valves that are suitable for use include, but are not limited to: a ball check valve; a diaphragm check valve; a butterfly check valve; a swing check valve; a duckbill valve; and a lift check valve. Under pressure, nitrogen molecules in the pressurized ambient air are adsorbed by the gas separation adsorbent in the pressurized canister. As the pressure increases, more nitrogen is adsorbed until the gas in the canister is enriched in oxygen. The nonadsorbed gas molecules (mainly oxygen) flow out of the pressurized canister when the pressure reaches a point sufficient to overcome the resistance of the check valve coupled to the canister. In one embodiment, the pressure drop of the check valve in the forward direction is less than 1 psi. The break pressure in the reverse direction is greater than 100 psi. It should be understood, however, that modification of one or more components would alter the operating parameters of these valves. If the forward flow pressure is increased, there is, generally, a reduction in oxygen enriched gas production. If the break pressure for reverse flow is reduced or set too low, there is, generally, a reduction in oxygen enriched gas pressure.

In an exemplary embodiment, canister 302 is pressurized by compressed air produced in compression system 200 and passed into canister 302. During pressurization of canister 302 inlet valve 122 is open, outlet valve 132 is closed, inlet valve 124 is closed and outlet valve 134 is open. Outlet valve 134 is opened when outlet valve 132 is closed to allow substantially simultaneous venting of canister 304 while canister 302 is pressurized. Canister 302 is pressurized until the pressure in canister is sufficient to open check valve 142. Oxygen enriched gas produced in canister 302 exits through check valve and, in one embodiment, is collected in accumulator 106.

After some time the gas separation adsorbent will become saturated with nitrogen and will be unable to separate significant amounts of nitrogen from incoming air. This point is usually reached after a predetermined time of oxygen enriched gas production. In the embodiment described above, when the gas separation adsorbent in canister 302 reaches this saturation point, the inflow of compressed air is stopped and canister 302 is vented to remove nitrogen. During venting, inlet valve 122 is closed, and outlet valve 132 is opened. While canister 302 is being vented, canister 304 is pressurized to produce oxygen enriched gas in the same manner described above. Pressurization of canister 304 is achieved by closing outlet valve 134 and opening inlet valve 124. The oxygen enriched gas exits canister 304 through check valve 144.

During venting of canister 302, outlet valve 132 is opened allowing pressurized gas (mainly nitrogen) to exit the canister through concentrator outlet 130. In an embodiment, the vented gases may be directed through muffler 133 to reduce the noise produced by releasing the pressurized gas from the canister. As gas is released from canister 302, pressure in the canister drops. The drop in pressure may allow the nitrogen to become desorbed from the gas separation adsorbent. The released nitrogen exits the canister through outlet 130, resetting the canister to a state that allows renewed separation of oxygen from an air stream. Muffler 133 may include open cell foam (or another material) to muffle the sound of the gas leaving the oxygen concentrator. In some embodiments, the combined muffling components/techniques for the input of air and the output of gas may provide for oxygen concentrator operation at a sound level below 50 decibels.

During venting of the canisters, it is advantageous that at least a majority of the nitrogen is removed. In an embodiment, at least about 50%, at least about 60%, at least about 70%, at least about 80%, at least about 90%, at least about 95%, at least about 98%, or substantially all of the nitrogen in a canister is removed before the canister is re-used to separate oxygen from air. In some embodiments, a canister may be further purged of nitrogen using an oxygen enriched stream that is introduced into the canister from the other canister.

In an exemplary embodiment, a portion of the oxygen enriched gas may be transferred from canister 302 to canister 304 when canister 304 is being vented of nitrogen. Transfer of oxygen enriched gas from canister 302 to 304, during venting of canister 304, helps to further purge nitrogen (and other gases) from the canister. In an embodiment, oxygen enriched gas may travel through flow restrictors 151, 153, and 155 between the two canisters. Flow restrictor 151 may be a trickle flow restrictor. Flow restrictor 151, for example, may be a 0.009 D flow restrictor (e.g., the flow restrictor has a radius of 0.009 inches which is less than the diameter of the tube it is inside). Flow restrictors 153 and 155 may be 0.013 D flow restrictors. Other flow restrictor types and sizes are also contemplated and may be used depending on the specific configuration and tubing used to couple the canisters. In some embodiments, the flow restrictors may be press fit flow restrictors that restrict air flow by introducing a narrower diameter in their respective tube. In some embodiments, the press fit flow restrictors may be made of sapphire, metal or plastic (other materials are also contemplated).

Flow of oxygen enriched gas is also controlled by use of valve 152 and valve 154. Valves 152 and 154 may be opened for a short duration during the venting process (and may be closed otherwise) to prevent excessive oxygen loss out of the purging canister. Other durations are also contemplated. In an exemplary embodiment, canister 302 is being vented and it is desirable to purge canister 302 by passing a portion of the oxygen enriched gas being produced in canister 304 into canister 302. A portion of oxygen enriched gas, upon pressurization of canister 304, will pass through flow restrictor 151 into canister 302 during venting of canister 302. Additional oxygen enriched air is passed into canister 302, from canister 304, through valve 154 and flow restrictor 155. Valve 152 may remain closed during the transfer process, or may be opened if additional oxygen enriched gas is needed. The selection of appropriate flow restrictors 151 and 155, coupled with controlled opening of valve 154 allows a controlled amount of oxygen enriched gas to be sent from canister 304 to 302. In an embodiment, the controlled amount of oxygen enriched gas is an amount sufficient to purge canister 302 and minimize the loss of oxygen enriched gas through venting valve 132 of canister 302. While this embodiment describes venting of canister 302, it should be understood that the same process can be used to vent canister 304 using flow restrictor 151, valve 152 and flow restrictor 153.

The pair of equalization/vent valves 152/154 work with flow restrictors 153 and 155 to optimize the air flow balance between the two canisters. This may allow for better flow control for venting the canisters with oxygen enriched gas from the other of the canisters. It may also provide better flow direction between the two canisters. It has been found that, while flow valves 152/154 may be operated as bi-directional valves, the flow rate through such valves varies depending on the direction of fluid flowing through the valve. For example, oxygen enriched gas flowing from canister 304 toward canister 302 has a flow rate faster through valve 152 than the flow rate of oxygen enriched gas flowing from canister 302 toward canister 304 through valve 152. If a single valve was to be used, eventually either too much or too little oxygen enriched gas would be sent between the canisters and the canisters would, over time, begin to produce different amounts of oxygen enriched gas. Use of opposing valves and flow restrictors on parallel air pathways may equalize the flow pattern of the oxygen between the two canisters. Equalizing the flow may allow for a steady amount of oxygen available to the user over multiple cycles and also may allow a predictable volume of oxygen to purge the other of the canisters. In some embodiments, the air pathway may not have restrictors but may instead have a valve with a built in resistance or the air pathway itself may have a narrow radius to provide resistance.

At times, an oxygen concentrator may be shut down for a period of time. When an oxygen concentrator is shut down, the temperature inside the canisters may drop as a result of the loss of adiabatic heat from the compression system. As the temperature drops, the volume occupied by the gases inside the canisters will drop. Cooling of the canisters may lead to a negative pressure in the canisters. Valves (e.g., valves 122, 124, 132, and 134) leading to and from the canisters are dynamically sealed rather than hermetically sealed. Thus, outside air may enter the canisters after shutdown to accommodate the pressure differential. When outside air enters the canisters, moisture from the outside air may condense inside the canister as the air cools. Condensation of water inside the canisters may lead to gradual degradation of the gas separation adsorbents, steadily reducing ability of the gas separation adsorbents to produce oxygen enriched gas.

In an embodiment, outside air may be inhibited from entering canisters after the oxygen concentrator is shut down by pressurizing both canisters prior to shut down. By storing the canisters under a positive pressure, the valves may be forced into a hermetically closed position by the internal pressure of the air in the canisters. In an embodiment, the pressure in the canisters, at shutdown, should be at least greater than ambient pressure. As used herein the term “ambient pressure” refers to the pressure of the surroundings that the oxygen generator is located (e.g. the pressure inside a room, outside, in a plane, etc.). In an embodiment, the pressure in the canisters, at shutdown, is at least greater than standard atmospheric pressure (i.e., greater than 760 mmHg (Torr), 1 atm, 101,325 Pa). In an embodiment, the pressure in the canisters, at shutdown, is at least about 1.1 times greater than ambient pressure; is at least about 1.5 times greater than ambient pressure; or is at least about 2 times greater than ambient pressure.

In an embodiment, pressurization of the canisters may be achieved by directing pressurized air into each canister from the compression system and closing all valves to trap the pressurized air in the canisters. In an exemplary embodiment, when a shutdown sequence is initiated, inlet valves 122 and 124 are opened and outlet valves 132 and 134 are closed. Because inlet valves 122 and 124 are joined together by a common conduit, both canisters 302 and 304 may become pressurized as air and or oxygen enriched gas from one canister may be transferred to the other canister. This situation may occur when the pathway between the compression system and the two inlet valves allows such transfer. Because the oxygen generator operates in an alternating pressurize/venting mode, at least one of the canisters should be in a pressurized state at any given time. In an alternate embodiment, the pressure may be increased in each canister by operation of compression system 200. When inlet valves 122 and 124 are opened, pressure between canisters 302 and 304 will equalize, however, the equalized pressure in either canister may not be sufficient to inhibit air from entering the canisters during shutdown. In order to ensure that air is inhibited from entering the canisters, compression system 200 may be operated for a time sufficient to increase the pressure inside both canisters to a level at least greater than ambient pressure. Regardless of the method of pressurization of the canisters, once the canisters are pressurized, inlet valves 122 and 124 are closed, trapping the pressurized air inside the canisters, which inhibits air from entering the canisters during the shutdown period.

An outlet system, coupled to one or more of the canisters, includes one or more conduits for providing oxygen enriched gas to a user. In an embodiment, oxygen enriched gas produced in either of canisters 302 and 304 is collected in accumulator 106 through check valves 142 and 144, respectively, as depicted schematically in FIG. 2. The oxygen enriched gas leaving the canisters may be collected in oxygen accumulator 106 prior to being provided to a user. In some embodiments, a tube may be coupled to accumulator 106 to provide the oxygen enriched gas to the user. Oxygen enriched gas may be provided to the user through an airway delivery device that transfer the oxygen enriched gas to the user's mouth and/or nose. In an embodiment, an outlet may include a tube that directs the oxygen toward a user's nose and/or mouth that may not be directly coupled to the user's nose.

Home oxygen concentrator may include many of the same components described above for portable oxygen concentrator. For example, may include a muffler 708, a compression system 770, canisters 730, an accumulator 735 and various valves and conduits, similar in function as described for a portable oxygen concentrator. Home oxygen concentrator 720 may function in the same manner as described above for portable concentrator, with regard to the production of oxygen enriched gas.

Turning to FIG. 3, a schematic diagram of an embodiment of an outlet system for portable oxygen concentrator 100 is shown. Supply valve 160 may be coupled to outlet tube to control the release of the oxygen enriched gas from accumulator 106 to the user. In an embodiment, supply valve 160 is an electromagnetically actuated plunger valve. Supply valve 160 is actuated by controller 400 to control the delivery of oxygen enriched gas to a user. Actuation of supply valve 160 is not timed or synchronized to the pressure swing adsorption process. Instead, actuation is, in some embodiments, synchronized to the patient's breathing. Additionally, supply valve 160 may have multiple actuations to help establish a clinically effective flow profile for providing oxygen enriched gas.

Oxygen enriched gas in accumulator 106 passes through supply valve 160 into expansion chamber 170 as depicted in FIG. 3. In an embodiment, expansion chamber may include one or more devices capable of being used to determine an oxygen concentration of gas passing through the chamber. Oxygen enriched gas in expansion chamber 170 builds briefly, through release of gas from accumulator by supply valve 160, and then is bled through small orifice flow restrictor 175 to flow rate sensor 185 and then to particulate filter 187. Flow restrictor 175 may be a 0.025 D flow restrictor. Other flow restrictor types and sizes may be used. In some embodiments, the diameter of the air pathway in the housing may be restricted to create restricted air flow. Flow rate sensor 185 may be any sensor capable of assessing the rate of gas flowing through the conduit. Particulate filter 187 may be used to filter bacteria, dust, granule particles, etc. prior to delivery of the oxygen enriched gas to the user. The oxygen enriched gas passes through filter 187 to connector 190 which sends the oxygen enriched gas to the user via conduit 192 and to pressure sensor 194.

The fluid dynamics of the outlet pathway, coupled with the programmed actuations of supply valve 160, results in a bolus of oxygen being provided at the correct time and with a flow profile that assures rapid delivery into the patient's lungs without any excessive flow rates that would result in wasted retrograde flow out the nostrils and into the atmosphere. It has been found, in our specific system, that the total volume of the bolus required for prescriptions is equal to 11 mL for each LPM, i.e., 11 mL for a prescription of 1 LPM; 22 mL for a prescription of 2 LPM; 33 mL for a prescription of 3 LPM; 44 mL for a prescription of 4 LPM; 55 mL for a prescription of 5 LPM; etc. This is generally referred to as the LPM equivalent. It should be understood that the LPM equivalent may vary between apparatus due to differences in construction design, tubing size, chamber size, etc.

Expansion chamber 170 may include one or more oxygen sensors capable of being used to determine an oxygen concentration of gas passing through the chamber. In an embodiment, the oxygen concentration of gas passing through expansion chamber 170 is assessed using oxygen sensor 165. An oxygen sensor is a device capable of detecting oxygen in a gas. Examples of oxygen sensors include, but are not limited to, ultrasonic oxygen sensors, electrical oxygen sensors, and optical oxygen sensors. In one embodiment, oxygen sensor 165 is an ultrasonic oxygen sensor that includes ultrasonic emitter 166 and ultrasonic receiver 168. In some embodiments, ultrasonic emitter 166 may include multiple ultrasonic emitters and ultrasonic receiver 168 may include multiple ultrasonic receivers. In embodiments having multiple emitters/receivers, the multiple ultrasonic emitters and multiple ultrasonic receivers may be axially aligned (e.g., across the gas mixture flow path which may be perpendicular to the axial alignment).

In use, an ultrasonic sound wave (from emitter 166) may be directed through oxygen enriched gas disposed in chamber 170 to receiver 168. Ultrasonic sensor assembly may be based on detecting the speed of sound through the gas mixture to determine the composition of the gas mixture (e.g., the speed of sound is different in nitrogen and oxygen). In a mixture of the two gases, the speed of sound through the mixture may be an intermediate value proportional to the relative amounts of each gas in the mixture. In use, the sound at the receiver 168 is slightly out of phase with the sound sent from emitter 166. This phase shift is due to the relatively slow velocity of sound through a gas medium as compared with the relatively fast speed of the electronic pulse through wire. The phase shift, then, is proportional to the distance between the emitter and the receiver and the speed of sound through the expansion chamber. The density of the gas in the chamber affects the speed of sound through the chamber and the density is proportional to the ratio of oxygen to nitrogen in the chamber. Therefore, the phase shift can be used to measure the concentration of oxygen in the expansion chamber. In this manner the relative concentration of oxygen in the accumulation chamber may be assessed as a function of one or more properties of a detected sound wave traveling through the accumulation chamber.

In some embodiments, multiple emitters 166 and receivers 168 may be used. The readings from the emitters 166 and receivers 168 may be averaged to cancel errors that may be inherent in turbulent flow systems. In some embodiments, the presence of other gases may also be detected by measuring the transit time and comparing the measured transit time to predetermined transit times for other gases and/or mixtures of gases.

The sensitivity of the ultrasonic sensor system may be increased by increasing the distance between emitter 166 and receiver 168, for example to allow several sound wave cycles to occur between emitter 166 and the receiver 168. In some embodiments, if at least two sound cycles are present, the influence of structural changes of the transducer may be reduced by measuring the phase shift relative to a fixed reference at two points in time. If the earlier phase shift is subtracted from the later phase shift, the shift caused by thermal expansion of expansion chamber 170 may be reduced or cancelled. The shift caused by a change of the distance between emitter 166 and receiver 168 may be the approximately the same at the measuring intervals, whereas a change owing to a change in oxygen concentration may be cumulative. In some embodiments, the shift measured at a later time may be multiplied by the number of intervening cycles and compared to the shift between two adjacent cycles. Further details regarding sensing of oxygen in the expansion chamber may be found, for example, in U.S. Published Patent Application No. 2009-0065007, published Mar. 12, 2009, and entitled “Oxygen Concentrator Apparatus and Method, which is incorporated herein by reference.

Flow rate sensor 185 may be used to determine the flow rate of gas flowing through the outlet system. Flow rate sensors that may be used include, but are not limited to: diaphragm/bellows flow meters; rotary flow meters (e.g. Hall Effect flow meters); turbine flow meters; orifice flow meters; and ultrasonic flow meters. Flow rate sensor 185 may be coupled to controller 400. The rate of gas flowing through the outlet system may be an indication of the breathing volume of the user. Changes in the flow rate of gas flowing through the outlet system may also be used to determine a breathing rate of the user. Controller 400 may control actuation of supply valve 160 based on the breathing rate and/or breathing volume of the user, as assessed by flow rate sensor 185

In some embodiments, ultrasonic sensor system 165 and, for example, flow rate sensor 185 may provide a measurement of an actual amount of oxygen being provided. For example, follow rate sensor 185 may measure a volume of gas (based on flow rate) provided and ultrasonic sensor system 165 may provide the concentration of oxygen of the gas provided. These two measurements together may be used by controller 400 to determine an approximation of the actual amount of oxygen provided to the user.

Oxygen enriched gas passes through flow meter 185 to filter 187. Filter 187 removes bacteria, dust, granule particles, etc. prior to providing the oxygen enriched gas to the user. The filtered oxygen enriched gas passes through filter 187 to connector 190. Connector 190 may be a “Y” connector coupling the outlet of filter 187 to pressure sensor 194 and outlet conduit 192. Pressure sensor 194 may be used to monitor the pressure of the gas passing through conduit 192 to the user. Changes in pressure, sensed by pressure sensor 194, may be used to determine a breathing rate of a user, as well as the onset of inhalation. Controller 400 may control actuation of supply valve 160 based on the breathing rate and/or onset of inhalation of the user, as assessed by pressure sensor 194. In an embodiment, controller 400 may control actuation of supply valve 160 based on information provided by flow rate sensor 185 and pressure sensor 194.

Oxygen enriched gas may be provided to a user through conduit 192. In an embodiment, conduit 192 may be a silicone tube. Conduit 192 may be coupled to a user using an airway coupling member 196, as depicted in FIG. 4. Airway coupling member 196 may be any device capable of providing the oxygen enriched gas to nasal cavities or oral cavities. Examples of airway coupling members include, but are not limited to: nasal masks, nasal pillows, nasal prongs, nasal cannulas, and mouthpieces. A nasal cannula airway delivery device is depicted in FIG. 4. During use, oxygen enriched gas from oxygen concentrator system 100 is provided to the user through conduit 192 and airway coupling member 196. Airway coupling member 196 is positioned proximate to a user's airway (e.g., proximate to the user's mouth and or nose) to allow delivery of the oxygen enriched gas to the user while allowing the user to breath air from the surroundings.

Canister System

Portable oxygen concentrator system 100 and home oxygen concentrator 720 include at least two canisters, each canister including a gas separation adsorbent. The canisters of either oxygen concentrator system may be disposed within a molded housing. In an embodiment, canister system 300 includes two housing components 310 and 510, as depicted in FIG. 5. The housing components 310 and 510 may be formed separately and then coupled together. In some embodiments, housing components 310 and 510 may be injection molded or compression molded. Housing components 310 and 510 may be made from a thermoplastic polymer such as polycarbonate, methylene carbide, polystyrene, acrylonitrile butadiene styrene (ABS), polypropylene, polyethylene, or polyvinyl chloride. In another embodiment, housing components 310 and 510 may be made of a thermoset plastic or metal (such as stainless steel or a light-weight aluminum alloy). Lightweight materials may be used to reduce the weight of the oxygen concentrator 100. In some embodiments, the two housings 310 and 510 may be fastened together using screws or bolts. Alternatively, housing components 310 and 510 may be solvent welded together.

As shown, valve seats 320, 322, 324, and 326 and air pathways 330 and 332 may be integrated into the housing component 310 to reduce the number of sealed connections needed throughout the air flow of the oxygen concentrator 100. In various embodiments, the housing components 310 and 410 of the oxygen concentrator 100 may form a two-part molded plastic frame that defines two canisters 302 and 304 and accumulation chamber 106.

Air pathways/tubing between different sections in housing components 310 and 510 may take the form of molded conduits. Conduits in the form of molded channels for air pathways may occupy multiple planes in housing components 310 and 510. For example, the molded air conduits may be formed at different depths and at different x,y,z positions in housing components 310 and 510. In some embodiments, a majority or substantially all of the conduits may be integrated into the housing components 310 and 510 to reduce potential leak points.

In some embodiments, prior to coupling housing components 310 and 510 together, O-rings may be placed between various points of housing components 310 and 510 to ensure that the housing components are properly sealed. In some embodiments, components may be integrated and/or coupled separately to housing components 310 and 510. For example, tubing, flow restrictors (e.g., press fit flow restrictors), oxygen sensors, gas separation adsorbents 139, check valves, plugs, processors, power supplies, etc. may be coupled to housing components 510 and 410 before and/or after the housing components are coupled together.

In some embodiments, apertures 337 leading to the exterior of housing components 310 and 410 may be used to insert devices such as flow restrictors. Apertures may also be used for increased moldability. One or more of the apertures may be plugged after molding (e.g., with a plastic plug). In some embodiments, flow restrictors may be inserted into passages prior to inserting plug to seal the passage. Press fit flow restrictors may have diameters that may allow a friction fit between the press fit flow restrictors and their respective apertures. In some embodiments, an adhesive may be added to the exterior of the press fit flow restrictors to hold the press fit flow restrictors in place once inserted. In some embodiments, the plugs may have a friction fit with their respective tubes (or may have an adhesive applied to their outer surface). The press fit flow restrictors and/or other components may be inserted and pressed into their respective apertures using a narrow tip tool or rod (e.g., with a diameter less than the diameter of the respective aperture). In some embodiments, the press fit flow restrictors may be inserted into their respective tubes until they abut a feature in the tube to halt their insertion. For example, the feature may include a reduction in radius. Other features are also contemplated (e.g., a bump in the side of the tubing, threads, etc.). In some embodiments, press fit flow restrictors may be molded into the housing components (e.g., as narrow tube segments).

In some embodiments, spring baffle 129 may be placed into respective canister receiving portions of housing component 310 and 510 with the spring side of the baffle 129 facing the exit of the canister. Spring baffle 129 may apply force to gas separation adsorbent 139 in the canister while also assisting in preventing gas separation adsorbent 139 from entering the exit apertures. Use of a spring baffle 129 may keep the gas separation adsorbent compact while also allowing for expansion (e.g., thermal expansion). Keeping the gas separation adsorbent 139 compact may prevent the gas separation adsorbent from breaking during movement of the oxygen concentrator system 100).

In some embodiments, pressurized air from the compression system 200 may enter air inlet 306. Air inlet 306 is coupled to inlet conduit 330. Air enters housing component 310 through inlet 306 travels through conduit 330, and then to valve seats 322 and 324. FIG. 6 and FIG. 7 depict an end view of housing 310. FIG. 6 depicts an end view of housing 310 prior to fitting valves to housing 310. FIG. 7 depicts an end view of housing 310 with the valves fitted to the housing 310. Valve seats 322 and 324 are configured to receive inlet valves 122 and 124 respectively. Inlet valve 122 is coupled to canister 302 and inlet valve 124 is coupled to canister 304. Housing 310 also includes valve seats 332 and 334 configured to receive outlet valves 132 and 134 respectively. Outlet valve 132 is coupled to canister 302 and outlet valve 134 is coupled to canister 304. Inlet valves 122/124 are used to control the passage of air from conduit 330 to the respective canisters.

In an embodiment, pressurized air is sent into one of canisters 302 or 304 while the other canister is being vented. For example, during use, inlet valve 122 is opened while inlet valve 124 is closed. Pressurized air from compression system 200 is forced into canister 302, while being inhibited from entering canister 304 by inlet valve 124. During pressurization of canister 302, outlet valve 132 is closed and outlet valve 134 is opened. Similar to the inlet valves, outlet valves 132 and 134 are operated out of phase with each other. Each inlet valve seat 322 includes an opening 375 that passes through housing 310 into canister 302. Similarly valve seat 324 includes an opening 325 that passes through housing 310 into canister 302. Air from conduit 330 passes through openings 323, or 325 if the respective valve (322 or 324) is open, and enters a canister.

Check valves 142 and 144 (See, FIG. 5) are coupled to canisters 302 and 304, respectively. Check valves 142 and 144 are one way valves that are passively operated by the pressure differentials that occur as the canisters are pressurized and vented. Oxygen enriched gas, produced in canisters 302 and 304 pass from the canister into openings 542 and 544 of housing 410. A passage (not shown) links openings 542 and 544 to conduits 342 and 344, respectively. Oxygen enriched gas produced in canister 302 passes from the canister though opening 542 and into conduit 342 when the pressure in the canister is sufficient to open check valve 142. When check valve 142 is open, oxygen enriched gas flows through conduit 342 toward the end of housing 310. Similarly, oxygen enriched gas produced in canister 304 passes from the canister though opening 544 and into conduit 344 when the pressure in the canister is sufficient to open check valve 144. When check valve 144 is open, oxygen enriched gas flows through conduit 344 toward the end of housing 310.

Oxygen enriched gas from either canister, travels through conduit 342 or 344 and enters conduit 346 formed in housing 310. Conduit 346 includes openings that couple the conduit to conduit 342, conduit 344 and accumulator 106. Thus oxygen enriched gas, produced in canister 302 or 304, travels to conduit 346 and passes into accumulator 106.

After some time the gas separation adsorbent will become saturated with nitrogen and will be unable to separate significant amounts of nitrogen from incoming air. When the gas separation adsorbent in a canister reaches this saturation point, the inflow of compressed air is stopped and the canister is vented to remove nitrogen. Canister 302 is vented by closing inlet valve 122 and opening outlet valve 132. Outlet valve 132 releases the vented gas from canister 302 into the volume defined by the end of housing 310. Foam material may cover the end of housing 310 to reduce the sound made by release of gases from the canisters. Similarly, canister 304 is vented by closing inlet valve 124 and opening outlet valve 134. Outlet valve 134 releases the vented gas from canister 304 into the volume defined by the end of housing 310.

While canister 302 is being vented, canister 304 is pressurized to produce oxygen enriched gas in the same manner described above. Pressurization of canister 304 is achieved by closing outlet valve 134 and opening inlet valve 124. The oxygen enriched gas exits canister 304 through check valve 144.

In an exemplary embodiment, a portion of the oxygen enriched gas may be transferred from canister 302 to canister 304 when canister 304 is being vented of nitrogen. Transfer of oxygen enriched gas from canister 302 to canister 304, during venting of canister 304, helps to further purge nitrogen (and other gases) from the canister. Flow of oxygen enriched gas between the canisters is controlled using flow restrictors and valves, as depicted in FIG. 2. Three conduits are formed in housing 510 for use in transferring oxygen enriched gas between canisters. As shown in FIG. 8, conduit 530 couples canister 302 to canister 304. Flow restrictor 151 (not shown) is disposed in conduit 530, between canister 302 and canister 304 to restrict flow of oxygen enriched gas during use. Conduit 532 also couples canister 302 to 304. Conduit 532 is coupled to valve seat 552 which receives valve 152, as shown in FIG. 9. Flow restrictor 153 (not shown) is disposed in conduit 532, between canister 302 and 304. Conduit 534 also couples canister 302 to 304. Conduit 534 is coupled to valve seat 554 which receives valve 154, as shown in FIG. 9. Flow restrictor 155 (not shown) is disposed in conduit 434, between canister 302 and 304. The pair of equalization/vent valves 152/154 work with flow restrictors 153 and 155 to optimize the air flow balance between the two canisters.

Oxygen enriched gas in accumulator 106 passes through supply valve 160 into expansion chamber 170 which is formed in housing 510. An opening (not shown) in housing 510 couples accumulator 106 to supply valve 160. In an embodiment, expansion chamber may include one or more devices capable of being used to determine an oxygen concentration of gas passing through the chamber.

Controller System

In one embodiment, operation of both portable oxygen concentrator system 100 and home oxygen concentrator 720 may be performed automatically using a controller 400 of the portable oxygen concentrator. In an embodiment, operation of portable oxygen concentrator system 100 and home oxygen concentrator 720 may be performed automatically using controllers 400 and 770, respectfully. Controller 400 includes one or more processors 410 and internal memory 420, as depicted in FIG. 2. Controller 770 includes one or more processors 772 and internal memory 774, as depicted in FIG. 2. Methods used to operate and monitor portable oxygen concentrator system 100 may be implemented by program instructions stored in memory 420 or a carrier medium coupled to controller 400, and executed by one or more processors 410. Methods used to operate and monitor portable oxygen concentrator system 720 may be implemented by program instructions stored in memory 774 or a carrier medium coupled to controller 720, and executed by one or more processors 772. A non-transitory memory medium may include any of various types of memory devices or storage devices. The term “memory medium” is intended to include an installation medium, e.g., a Compact Disc Read Only Memory (CD-ROM), floppy disks, or tape device; a computer system memory or random access memory such as Dynamic Random Access Memory (DRAM), Double Data Rate Random Access Memory (DDR RAM), Static Random Access Memory (SRAM), Extended Data Out Random Access Memory (EDO RAM), Rambus Random Access Memory (RAM), etc.; or a non-volatile memory such as a magnetic media, e.g., a hard drive, or optical storage. The memory medium may comprise other types of memory as well, or combinations thereof In addition, the memory medium may be located in a first computer in which the programs are executed, or may be located in a second different computer that connects to the first computer over a network, such as the Internet. In the latter instance, the second computer may provide program instructions to the first computer for execution. The term “memory medium” may include two or more memory mediums that may reside in different locations, e.g., in different computers that are connected over a network.

In some embodiments, processors 410 and 772 include, for example, one or more field programmable gate arrays (FPGAs), microcontrollers, etc. included on a circuit board disposed in the respective oxygen concentrator system. Processors 410/772 are capable of executing programming instructions stored in memory. In some embodiments, programming instructions may be built into the processors such that a memory external to the processor may not be separately accessed (i.e., the memory may be internal to the processor).

Processor 410 may be coupled to various components of oxygen concentrator system 100, including, but not limited to compression system 200, one or more of the valves used to control fluid flow through the system (e.g., valves 122, 124, 132, 134, 152, 154, 160, or combinations thereof), oxygen sensor 165, pressure sensor 194, flow rate monitor 180, temperature sensors, fans, and any other component that may be electrically controlled. Processor 410 may also be coupled to processor 770 of home oxygen concentrator 720, when the portable oxygen concentrator is coupled to the home oxygen concentrator.

In an embodiment, controller 770 controls the operation of home oxygen concentrator 720. Processor 770 may be coupled to various components of oxygen concentrator system 720, including, but not limited to compression system 780, one or more of the valves used to control fluid flow through the system, oxygen sensor 165, pressure sensor 194, flow rate monitor 180, temperature sensors, fans, and any other component that may be electrically controlled. Controller 770 is capable of operating home oxygen concentrator 720 by itself, or in combination with processor 410 of portable oxygen concentrator 100. For example, when a portable oxygen concentrator is not coupled to the home oxygen concentrator, operation of the home oxygen concentrator is controlled by controller 770. Operating parameters (valve timings, oxygen delivery, compressor operation, etc.) may be stored in controller memory 774 and be used to operate the home oxygen concentrator. Operation of home oxygen concentrator may be optimized by the operating parameters, to deliver oxygen enriched gas to a user in a manner that is consistent with the supplemental oxygen required by the user.

In an embodiment, the operating parameters of home oxygen concentrator 720 are set by portable oxygen concentrator 100 when the portable oxygen concentrator is coupled to the home oxygen concentrator. Thus one set of patient specific oxygen enriched gas delivery parameters may be used to operate both the portable oxygen concentrator and the home oxygen concentrator. During typical use of the hybrid system a user of the system will usually have the portable oxygen concentrator with them at all times. Thus the most updated patient specific oxygen enriched gas delivery parameters should be stored on the portable oxygen concentrator. The home oxygen concentrator will also need the same patient specific oxygen enriched gas delivery parameters. In a less optimal configuration, the patient specific oxygen enriched gas delivery parameters would need to be separately updated on both the portable oxygen concentrator and the home oxygen concentrator anytime there is a change in the parameters. In an embodiment, this inconvenience can be eliminated by having the patient specific oxygen enriched gas delivery parameters transferred to the home oxygen concentrator when the portable oxygen concentrator is coupled to the home oxygen concentrator. Thus, if the patient specific oxygen enriched gas delivery parameters are changed, the change only needs to be made in the controller of the portable oxygen concentrator. When the portable oxygen concentrator is coupled to the home oxygen concentrator, the patient specific oxygen enriched gas delivery parameters are transferred to the home oxygen concentrator. In this manner the home oxygen concentrator is automatically updated to match the patient specific oxygen enriched gas delivery parameters of the portable oxygen concentrator. This helps to ensure consistent delivery of oxygen enriched gas to the patient. In one embodiment, the portable oxygen concentrator includes a port (e.g., a USB port) which allows connection of the portable oxygen concentrator to a computer. The computer may include software that allows the operating parameters of the portable oxygen concentrator and/or the home oxygen concentrator to be modified by the user or a medical professional.

In an embodiment, portable oxygen concentrator controller may also collect diagnostic data from the home oxygen concentrator for determining the operating state of the home oxygen concentrator. For example, portable oxygen concentrator may collect information regarding: purity of oxygen being produced; pressure of the canisters, temperature of the interior of the home oxygen concentrator, temperature of various components of the home oxygen concentrator, flow rate of gas through various conduits of the home oxygen concentrator, length of time the adsorbent has been in use, etc. These parameters may be analyzed by portable oxygen concentrator controller, or a host computer, when the portable oxygen concentrator is coupled to a computer, to determine if the home oxygen concentrator is operating correctly. If the home oxygen concentrator is not operating within acceptable parameters, the portable oxygen concentrator may change the operating parameters stored in the home oxygen concentrator controller, to compensate for the current condition of the home oxygen concentrator. For example, if the purity of oxygen drops below a predetermined amount (e.g., less than 95% pure) the valve timing may be adjusted to reduce the time the canisters are used to produce oxygen, thus minimizing the amount of nitrogen breakthrough which lowers the purity of the produced oxygen. Adjustment of the valve timing may be done when the portable oxygen concentrator is coupled to the home oxygen concentrator by transferring the required information to the home oxygen concentrator controller. Thus, when the home oxygen concentrator is operated in the absence of the portable oxygen concentrator, the adjusted operating parameters are used.

The specific valve timings and compressor speeds are typically not user adjustable parameters. These parameters, along with other parameters, may be adjusted by coupling the portable oxygen concentrator, which has collected diagnostic information from the home oxygen concentrator, to a computer. The computer may include software which analyzes the diagnostic information and prepares a set of new operating parameters which are stored on the portable oxygen concentrator for transfer to the home oxygen concentrator. Alternatively, the user may connect the portable oxygen concentrator to a computer and connect to the manufacturer's software applications via the internet. In either embodiment, the portable oxygen concentrator then transfers the operating parameters transferred from the software application to the home oxygen concentrator to adjust the home oxygen concentrator parameters.

In some embodiments, the computer may determine that one or more components (e.g., the adsorbent) of the home oxygen concentrator (or the portable oxygen concentrator) need to be replaced. The computer may provide a notification that the home oxygen concentrator (or portable oxygen concentrator) is in need a service when a component needs to be replaced.

Controller 400 of the portable oxygen concentrator is programmed to operate portable oxygen concentrator system 100, home oxygen concentrator 720 and is further programmed to monitor one or both oxygen concentrator systems for malfunction states. For example, in one embodiment, controller 400 is programmed to trigger an alarm if either system is operating and no breathing is detected by the user for a predetermined amount of time. For example, if controller 400 does not detect a breath for a period of 75 seconds, an alarm LED may be lit and/or an audible alarm may be sounded. If the user has truly stopped breathing, for example, during a sleep apnea episode, the alarm may be sufficient to awaken the user, causing the user to resume breathing. The action of breathing may be sufficient for controller 400 to reset this alarm function. Alternatively, if the system is accidently left on when output conduit 192 is removed from the user, the alarm may serve as a reminder for the user to turn oxygen concentrator system 100 off.

Controller 400 is further coupled to oxygen sensor 165, and may be programmed for continuous or periodic monitoring of the oxygen concentration of the oxygen enriched gas passing through expansion chamber 170. A minimum oxygen concentration threshold may be programmed into controller 400, such that the controller lights an LED visual alarm and/or an audible alarm to warn the patient of the low concentration of oxygen.

Controller 400 is also coupled to internal power supply 180 and is capable of monitoring the level of charge of the internal power supply. A minimum voltage and/or current threshold may be programmed into controller 400, such that the controller lights an LED visual alarm and/or an audible alarm to warn the patient of low power condition. The alarms may be activated intermittently and at an increasing frequency as the battery approaches zero usable charge.

Further functions of controller 400 are described in detail in other sections of this disclosure.

A user may have a low breathing rate or depth if relatively inactive (e.g., asleep, sitting, etc.) as assessed by comparing the detected breathing rate or depth to a threshold. The user may have a high breathing rate or depth if relatively active (e.g., walking, exercising, etc.). An active/sleep mode may be assessed automatically and/or the user may manually indicate a respective active or sleep mode by a pressing button for active mode and another button for sleep mode. In some embodiments, a user may toggle a switch from active mode, normal mode, or sedentary mode. The adjustments made by the oxygen concentrator system in response to activating active mode or sleep mode are described in more detail herein.

Methods of Delivery of Oxygen Enriched Gas

The main use of an oxygen concentrator system is to provide supplemental oxygen to a user. Generally, the amount of supplemental oxygen to be provided is assessed by a physician. Typical prescribed amounts of supplemental oxygen may range from about 1 LPM to up to about 10 LPM. The most commonly prescribed amounts are 1 LPM, 2 LPM, 3 LPM, and 4 LPM. Generally, oxygen enriched gas is provided to the use during a breathing cycle to meet the prescription requirement of the user. As used herein the term “breathing cycle” refers to an inhalation followed by an exhalation of a person.

In order to minimize the amount of oxygen enriched gas that is needed to be produced to meet the prescribed amounts, controller 400 may be programmed to time delivery of the oxygen enriched gas with the user's inhalations. Releasing the oxygen enriched gas to the user as the user inhales may prevent unnecessary oxygen generation (further reducing power requirements) by not releasing oxygen, for example, when the user is exhaling. Reducing the amount of oxygen required may effectively reduce the amount of air compressing needed for oxygen concentrator 100 (and subsequently may reduce the power demand from the compressors).

Oxygen enriched gas, produced by oxygen concentrator system 100 is stored in an oxygen accumulator 106 and released to the user as the user inhales. The amount of oxygen enriched gas provided by the oxygen concentrator system is controlled, in part, by supply valve 160. In an embodiment, supply valve 160 is opened for a sufficient amount of time to provide the appropriate amount of oxygen enriched gas, as assessed by controller 400, to the user. In order to minimize the amount of oxygen required to meet the prescription requirements of a user, the oxygen enriched gas may be provided in a bolus when a user's inhalation is first detected. For example, the bolus of oxygen enriched gas may be provided in the first few milliseconds of a user's inhalation.

In an embodiment, pressure sensor 194 and/or flow rate sensor 185 may be used to determine the onset of inhalation by the user. For example, the user's inhalation may be detected by using pressure sensor 194. In use, a conduit for providing oxygen enriched gas is coupled to a user's nose and/or mouth (e.g., using a nasal cannula or a face mask). At the onset of an inhalation, the user begins to draw air into their body through the nose and/or mouth. As the air is drawn in, a negative pressure is generated at the end of the conduit, due, in part, to the venturi action of the air being drawn across the end of the delivery conduit. Pressure sensor 194 may be operable to create a signal when a drop in pressure is detected, to signal the onset of inhalation. Upon detection of the onset of inhalation, supply valve 160 is controlled to release a bolus of oxygen enriched gas from the accumulator 106.

In some embodiments, pressure sensor 194 may provide a signal that is proportional to the amount of positive or negative pressure applied to a sensing surface. The amount of the pressure change detected by pressure sensor 194 may be used to refine the amount of oxygen enriched gas being provided to the user. For example, if a large negative pressure change is detected by pressure sensor 194, the volume of oxygen enriched gas provided to the user may be increased to take into account the increased volume of gas being inhaled by the user. If a smaller negative pressure is detected, the volume of oxygen enriched gas provided to the user may be decreased to take into account the decreased volume of gas being inhaled by the user. A positive change in the pressure indicates an exhalation by the user and is generally a time that release of oxygen enriched gas is discontinued. Generally while a positive pressure change is sensed, valve 160 remains closed until the next onset of inhalation.

In some embodiments, the sensitivity of the pressure sensor 194 may be affected by the physical distance of the pressure sensor 194 from the user, especially if the pressure sensor is located in oxygen concentrator system 100 and the pressure difference is detected through the tubing coupling the oxygen concentrator system to the user. In some embodiments, the pressure sensor may be placed in the airway delivery device used to provide the oxygen enriched gas to the user. A signal from the pressure sensor may be provided to controller 400 in the oxygen concentrator 100 electronically via a wire or through telemetry such as through BLUETOOTH® (Bluetooth, SIG, Inc. Kirkland, Wash.) or other wireless technology.

In an embodiment, the user's inhalation may be detected by using flow rate sensor 185. In use, a conduit for providing oxygen enriched gas is coupled to a user's nose and/or mouth (e.g., using a nasal cannula or face mask). At the onset of an inhalation, the user begins to draw air into their body through the nose and/or mouth. As the air is drawn in, an increase in flow of gas passing through conduit is created. Flow rate sensor 185 may be operable to create a signal when an increase in flow rate is detected, to signal the onset of inhalation. Upon detection of the onset of inhalation, supply valve 160 is controlled to release a bolus of oxygen enriched gas from the accumulator 106.

A user breathing at a rate of 30 breaths per minute (BPM) during an active state (e.g., walking, exercising, etc.) may consume two and one-half times as much oxygen as a user who is breathing at 12 BPM during a sedentary state (e.g., asleep, sitting, etc.). Pressure sensor 194 and/or flow rate sensor 185 may be used to determine the breathing rate of the user. Controller 400 may process information received from pressure sensor 194 and/or flow rate sensor 185 and determine a breathing rate based on the frequency of the onset of inhalation. The detected breathing rate of the user may be used to adjust the bolus of oxygen enriched gas. The volume of the bolus of oxygen enriched gas may be increased as the users breathing rate increase, and may be decreased as the users breathing rate decreases. Controller 400 may automatically adjust the bolus based on the detected activity state of the user. Alternatively, the user may manually indicate a respective active or sedentary mode by selecting the appropriate option on the control panel of the oxygen concentrator. Alternatively, a user may operate controller 400 from a remote electronic device. For example, a user may operate the controller using a smart phone or tablet device.

In some embodiments, if the user's current activity level as assessed using the detected user's breathing rate exceeds a predetermined threshold, controller 400 may implement an alarm (e.g., visual and/or audio) to warn the user that the current breathing rate is exceeding the delivery capacity of the oxygen concentrator system. For example, the threshold may be set at 20 breaths per minute.

In some embodiments, as seen in FIG. 9, the bolus of provided oxygen enriched gas may include two or more pulses. For example, with a one liter per minute (LPM) delivery rate, the bolus may include two pulses: a first pulse 556 at approximately 7 cubic centimeters and a second pulse 558 at approximately 3 cubic centimeters. Other delivery rates, pulse sizes, and number of pulses are also contemplated. For example, at 2 LPMs, the first pulse may be approximately 14 cubic centimeters and a second pulse may be approximately 6 cubic centimeters and at 3 LPMs, the first pulse may be approximately 21 cubic centimeters and a second pulse may be approximately 9 cubic centimeters. In some embodiments, the larger pulse 556 may be provided when the onset of inhalation is detected (e.g., detected by pressure sensor 194). In some embodiments, the pulses may be provided when the onset of inhalation is detected and/or may be spread time-wise evenly through the breath. In some embodiments, the pulses may be stair-stepped through the duration of the breath. In some embodiments, the pulses may be distributed in a different pattern. Additional pulses may also be used (e.g., 3, 4, 5, etc. pulses per breath). While the first pulse 556 is shown to be approximately twice the second pulse 558, in some embodiments, the second pulse 558 may be larger than the first pulse 556. In some embodiments, pulse size and length may be controlled by, for example, supply valve 160 which may open and close in a timed sequence to provide the pulses. A bolus with multiple pulses may have a smaller impact on a user than a bolus with a single pulse. The multiple pulses may also result in less drying of a user's nasal passages and less blood oxygen desaturation. The multiple pulses may also result in less oxygen waste.

In some embodiments, the sensitivity of the oxygen concentrator 100 may be selectively attenuated to reduce false inhalation detections due to movement of air from a different source (e.g., movement of ambient air). For example, the oxygen concentrator 100 may have two selectable modes—an active mode and an inactive mode. In some embodiments, the user may manually select a mode (e.g., through a switch or user interface). In some embodiments, the mode may be automatically selected by the oxygen concentrator 100 based on a detected breathing rate. For example, the oxygen concentrator 100 may use the pressure sensor 194 to detect a breathing rate of the user. If the breathing rate is above a threshold, the oxygen concentrator 100 may operate in an active mode (otherwise, the oxygen concentrator may operate in an inactive mode). Other modes and thresholds are also contemplated.

In some embodiments, in active mode, the sensitivity of the pressure sensor 194 may be mechanically, electronically, or programmatically attenuated. For example, during active mode, controller 400 may look for a greater pressure difference to indicate the start of a user breath (e.g., an elevated threshold may be compared to the detected pressure difference to determine if the bolus of oxygen should be released). In some embodiments, the pressure sensor 194 may be mechanically altered to be less sensitive to pressure differences. In some embodiments, an electronic signal from the pressure sensor may be electronically altered to ignore small pressure differences. This can be useful when in active mode. In some embodiments, during the inactive mode the sensitivity of the pressure sensor may be increased. For example, the controller 400 may look for a smaller pressure difference to indicate the start of a user breath (e.g., a smaller threshold may be compared to the detected pressure difference to determine if the bolus of oxygen should be released). In some embodiments, with increased sensitivity, the response time for providing the bolus of oxygen during the user's inhalation may be reduced. The increased sensitivity and smaller response time may reduce the size of the bolus necessary for a given flow rate equivalence. The reduced bolus size may also reduce the size and power consumption of the oxygen concentrator 100.

Providing a Bolus Based on Inhalation Profile

In an embodiment, the bolus profile can be designed to match the profile of a particular user. To do so, an inhalation profile may be generated based on information gathered from pressure sensor 194 and flow rate sensor 185. An inhalation profile is assessed based on, one or more of the following parameters: the breathing rate of the user; the inhalation volume of the user; the exhalation volume of the user; the inhalation flow rate of the user; and the exhalation flow rate of the user. The breathing rate of the user may be assessed by detecting the onset of inhalation using pressure sensor 194 or flow rate sensor 185 as previously discussed. Inhalation volume may be assessed by measuring the change in pressure during inhalation and calculating or empirically assessing the inhalation volume based on the change in pressure. Alternatively, inhalation volume may be assessed by measuring the flow rate during inhalation and calculating or empirically assessing the inhalation volume based on the flow rate and the length of the inhalation. Exhalation volume may be assessed in a similar manner using either positive pressure changes during exhalation, or flow rate and exhalation time. Inhalation flow rate of the user is measured from shortly after the onset of inhalation. Detection of the end of inhalation may be from the pressure sensor or the flow rate sensor. When onset of inhalation is detected by the pressure sensor, the onset is characterized by a drop in pressure. When the pressure begins to increase, the inhalation is considered complete. When onset of inhalation is detected by the flow rate sensor, the onset is characterized by an increase in the flow rate. When the flow rate begins to decrease, the inhalation is considered complete.

There is a minimum amount of oxygen necessary for a person to remain conscious. A person who is breathing rapidly is bringing in a lower volume of air in each breath, and thus, requires less oxygen enriched gas per inhalation. While there is some variation from patient to patient, this relationship can be used to establish the mean flow rate for each breath mathematically. By measuring a large population of patients, the profile of the relative flow from onset of inhalation to the onset of exhalation may be established. Using this flow profile as a template, the calculated actual flow based on breathing rate can be adjusted mathematically to a calculated actual flow profile. This profile can be used to adjust the opening and closing of the delivery valve to create an idealized profile for the patient based on their breathing rate. Inhalation profile data gathered from a population of users may be used to create an algorithm that makes the appropriate adjustments based on the detected inhalation profile. Alternatively, a look up table may be used to control valve actuation durations and pulse quantities based on a detected inhalation profile.

Measuring the inhalation profile of the patient provides a more accurate basis for control of the bolus of oxygen enriched gas being provided to the patient. For example, basing the delivery of oxygen enriched gas on the onset of inhalation may not take into account differences between individual users. For example, people having a similar breathing rate can have different inhalation/exhalation volume, inhalation/exhalation flow rates and, thus, different bolus requirements necessary to produce the prescribed amount of oxygen. In one embodiment, an inhalation profile is created based on the flow rate of air during inhalation and the duration of inhalation. The inhalation profile can then be used as a predictor of the volume of air taken in by a specific user during inhalation. Thus, inhalation profile information can be used to modify the amount of oxygen enriched air provided to the user to ensure that the prescribed level of oxygen is received. The amount of oxygen provided to a user may be adjusted by modifying the frequency and or duration of release of oxygen enriched gas from the accumulator with supply valve 160. By tracking the inhalation profile of the patient controller adjusts the delivery supply valve actuation to idealize the bolus profile to provide the oxygen at the maximum rate without causing wasteful retrograde flow.

FIG. 11 depicts an alternate schematic diagram of a portable oxygen concentrator 100 coupled to home oxygen concentrator 720. Portable oxygen concentrator 100 includes compression system 200, however home oxygen concentrator 720 does not include a compressor. Compression system 200 may produce compressed air and send compressed air to valve 720. Valve 720 controls the flow of compressed air to the portable oxygen concentrator or to conduit 765, which conducts the compressed air to home oxygen concentrator 720. In this construction, compression system 200 can send air to canisters 302, 304 of portable oxygen concentrator 100 and/or to canisters 730 of stationary oxygen concentrator 720. Valve 760 may be a three-way valve or any other known valve suitable to control air flow. Valve 760 may be controlled by controller 400. When using the hybrid oxygen concentrator apparatus 720, a user may select to use oxygen produced from portable oxygen concentrator 100 and/or stationary oxygen concentrator 620.

In another embodiment, a home oxygen concentrator 800 may be operated without a portable oxygen concentrator, as shown in FIG. 12. In this embodiment, a home oxygen concentrator 800 may include: at least two canisters, gas separation adsorbent disposed in at least two of the canisters, a compression system, and one or more conduits coupling the canisters to each other, and one or more valves coupled to the conduits. A controller 820 may be removably coupled to home oxygen concentrator 800. Controller 820 may provide control instructions to the compressor and valves to generate oxygen enriched gas from air sent into the canisters by the compression system, in a manner as described above. Controller 820 may take the place of a portable oxygen concentrator controller.

In some embodiments, controller 820 is couplable to both a home oxygen concentrator and a portable oxygen concentrator. Controller 820 may be programmed with the customized prescription information for the user. When the user switches from a home oxygen concentrator to a portable oxygen concentrator, the user may remove controller 820 from the home oxygen concentrator and place the controller in a suitable receptacle of a portable oxygen concentrator. In this manner, the prescription information of the patient may be transferred from one device to the other, without the need to program each device independently.

In an embodiment, controller 820 may include a wireless receiver and/or transmitter. The wireless receiver and/or transmitter may be used to transmit control signals to the home oxygen concentrator or a portable oxygen concentrator when either system is within the transmitter/receiver operating range. In one embodiment, the home oxygen concentrator may be controlled by transmitting a wireless signal from controller 820 to a sub-controller of the first oxygen concentrator. Controller 820 may also be used to operate a portable oxygen concentrator by providing wireless control signals to the portable oxygen concentrator.

In this patent, certain U.S. patents, U.S. patent applications, and other materials (e.g., articles) have been incorporated by reference. The text of such U.S. patents, U.S. patent applications, and other materials is, however, only incorporated by reference to the extent that no conflict exists between such text and the other statements and drawings set forth herein. In the event of such conflict, then any such conflicting text in such incorporated by reference U.S. patents, U.S. patent applications, and other materials is specifically not incorporated by reference in this patent.

Further modifications and alternative embodiments of various aspects of the invention may be apparent to those skilled in the art in view of this description. Accordingly, this description is to be construed as illustrative only and is for the purpose of teaching those skilled in the art the general manner of carrying out the invention. It is to be understood that the forms of the invention shown and described herein are to be taken as embodiments. Elements and materials may be substituted for those illustrated and described herein, parts and processes may be reversed, and certain features of the invention may be utilized independently, all as would be apparent to one skilled in the art after having the benefit of this description of the invention. Changes may be made in the elements described herein without departing from the spirit and scope of the invention as described in the following claims. 

What is claimed is:
 1. A method of producing oxygen enriched gas, comprising: coupling a first oxygen concentrator apparatus to a second oxygen concentrator apparatus, the first oxygen concentrator apparatus comprising: at least two canisters; gas separation adsorbent disposed in the at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a first apparatus controller that controls operation of the first oxygen concentrator apparatus using operating parameters stored in the first apparatus controller; the second oxygen concentrator apparatus comprising: at least two canisters; gas separation adsorbent disposed in the at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a second apparatus controller that controls operation of the second oxygen concentrator apparatus using operating parameters stored in the second apparatus controller; and wherein the first apparatus controller is coupled to the second apparatus controller when the first oxygen concentrator apparatus is coupled to the second oxygen concentration apparatus; altering the operating parameters of the second apparatus controller based on the operating parameters of the first apparatus controller when the first oxygen concentrator system is coupled to the second oxygen concentrator system, wherein the operating parameters of the second apparatus controller are altered by the first apparatus controller.
 2. The method of claim 1, further comprising regenerating gas adsorbent in the first oxygen concentrator apparatus while providing oxygen enriched gas to the user from the second oxygen apparatus.
 3. The method of claim 1, further comprising controlling the first and second oxygen concentrator apparatus using the first apparatus controller.
 4. The method of claim 1, further comprising controlling the first and second oxygen concentrator apparatus by transmitting a signal from a wireless controller to the first apparatus controller and/or the second apparatus controller.
 5. The method of claim 1, further comprising collecting diagnostic information regarding the operation of the first oxygen concentrator apparatus using the first apparatus controller; and collecting diagnostic information regarding the operation of the second oxygen concentrator apparatus with the first apparatus controller, when the first oxygen concentrator apparatus is coupled to the second oxygen concentrator apparatus.
 6. The method of claim 1, further comprising a coupling system with one or more conduits that couple the compressor of the first oxygen concentrator apparatus to one or more of the canisters of the second oxygen concentrator apparatus, wherein the method further comprises operating the compressor of the first oxygen concentrator apparatus to provide compressed air to one or more of the conduits of the second oxygen concentrator apparatus when the first oxygen concentrator apparatus is coupled to the second oxygen concentrator apparatus.
 7. The method of claim 1, further comprising decoupling the first oxygen concentrator apparatus from the second oxygen concentrator apparatus and coupling a portable controller to the second oxygen concentrator apparatus via the coupling system, wherein the portable controller operates the second oxygen concentrator apparatus.
 8. The method of claim 1, wherein the second oxygen concentrator apparatus further comprises one or more conduits that couple the outlet of one or more canisters of the second oxygen concentration apparatus to the first oxygen concentrator apparatus such that oxygen enriched gas is provided to the first oxygen concentrator apparatus from the second oxygen concentrator apparatus.
 9. The method of claim 1, wherein the second oxygen concentrator apparatus further comprises an oxygen enriched gas storage container and one or more conduits that couple the oxygen enriched gas storage container to the first oxygen concentrator apparatus, wherein the method further comprises providing oxygen enriched gas to the first oxygen concentrator apparatus from the oxygen enriched gas storage container.
 10. The method of claim 6, wherein the one or more conduits couple the outlet of one or more canisters of the second oxygen concentration apparatus to an outlet conduit of the first oxygen concentration apparatus that provides oxygen to a user of the first oxygen concentrator apparatus.
 11. The method of claim 1, further comprising a coupling system with a support structure which has a size and shape complementary to the size and shape of the first oxygen concentrator apparatus, and wherein coupling the first oxygen concentrator apparatus to the second oxygen concentrator apparatus comprises placing the first oxygen concentrator apparatus at least partially within the support structure.
 12. The method of claim 1, wherein patient specific oxygen enriched gas delivery parameters are stored on the first apparatus controller, and wherein the method further comprises altering the operating parameters of the second apparatus controller using the first apparatus controller such that oxygen enriched gas produced and delivered by the second oxygen concentrator apparatus corresponds to the patient specific oxygen enriched gas delivery parameters.
 13. An oxygen concentrator system, comprising: a first oxygen concentrator apparatus, the first oxygen concentrator apparatus comprising: at least two canisters; gas separation adsorbent disposed in the at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; and a first apparatus controller that controls the operation of the first oxygen concentrator apparatus; a second oxygen concentrator apparatus, the second oxygen concentrator apparatus comprising: at least two canisters; gas separation adsorbent disposed in the at least two canisters, wherein the gas separation adsorbent separates at least some nitrogen from air in the canister to produce oxygen enriched gas; a compression system comprising at least one compressor coupled to at least one canister; a second apparatus controller that controls the operation of the second oxygen concentrator apparatus using operating parameters stored in the second apparatus controller; and a coupling system that couples the first apparatus controller to the second apparatus controller; wherein the first apparatus controller alters the operating parameters of the second apparatus controller when coupled to the second apparatus controller.
 14. The oxygen concentrator system of claim 13, wherein the first apparatus controller collects diagnostic information regarding the operation of the first oxygen concentrator apparatus; and wherein the first apparatus controller collects diagnostic information regarding the operation of the second oxygen concentrator apparatus, when coupled to the second apparatus controller.
 15. The oxygen concentrator system of claim 14, wherein the first apparatus controller is coupleable to a computer system, wherein the computer system: analyzes the collected diagnostic information; determines new operating parameters for the first oxygen concentrator apparatus and/or the second oxygen concentrator apparatus; and stores the new operating parameters for the first oxygen concentrator apparatus and/or the second oxygen concentrator apparatus on the first apparatus controller.
 16. The oxygen concentrator system of claim 15, wherein the first apparatus controller changes the operating parameters stored on the second apparatus controller to the new operating parameters prepared by the computer system for the second oxygen concentrator apparatus when the first apparatus controller is coupled to the second apparatus controller.
 17. The oxygen concentrator system of claim 13, wherein second oxygen concentrator apparatus comprises a support structure which has a size and shape complementary to the size and shape of the first oxygen concentrator apparatus, and wherein the first oxygen concentrator apparatus fits at least partially within the support structure.
 18. The oxygen concentrator system of claim 13, wherein patient specific oxygen enriched gas delivery parameters are stored on the first apparatus controller, and wherein the first apparatus controller alters the operating parameters of the second apparatus controller such that oxygen enriched gas is produced and delivered by the second oxygen concentrator apparatus corresponds to the patient specific oxygen enriched gas delivery parameters.
 19. The oxygen concentrator system of claim 13, wherein the second oxygen concentrator system further comprises one or more conduits that couple the outlet of one or more canisters of the second oxygen concentration apparatus to the first oxygen concentrator apparatus such that oxygen enriched gas is provided to the first oxygen concentrator apparatus from the second oxygen concentrator apparatus.
 20. The oxygen concentrator system of claim 19, wherein the one or more conduits couple the outlet of one or more canisters of the second oxygen concentration apparatus to an outlet conduit of the first oxygen concentration apparatus that provides oxygen to a user of the first oxygen concentrator system. 